EP3620485A1 - Procédé de fabrication d'une matière de moulage à propriétés améliorées - Google Patents

Procédé de fabrication d'une matière de moulage à propriétés améliorées Download PDF

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Publication number
EP3620485A1
EP3620485A1 EP18192339.2A EP18192339A EP3620485A1 EP 3620485 A1 EP3620485 A1 EP 3620485A1 EP 18192339 A EP18192339 A EP 18192339A EP 3620485 A1 EP3620485 A1 EP 3620485A1
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EP
European Patent Office
Prior art keywords
sub
polycarbonate
molding composition
reinforcing filler
titanium dioxide
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
EP18192339.2A
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German (de)
English (en)
Inventor
Erfindernennung liegt noch nicht vor Die
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Covestro Deutschland AG
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Covestro Deutschland AG
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Publication date
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Priority to EP18192339.2A priority Critical patent/EP3620485A1/fr
Priority to EP19752533.0A priority patent/EP3847210A1/fr
Priority to KR1020217005858A priority patent/KR20210055683A/ko
Priority to PCT/EP2019/071893 priority patent/WO2020048750A1/fr
Priority to CN201980057499.0A priority patent/CN112823185A/zh
Priority to US17/268,560 priority patent/US20210316491A1/en
Publication of EP3620485A1 publication Critical patent/EP3620485A1/fr
Ceased legal-status Critical Current

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    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00—Use of inorganic substances as compounding ingredients
    • C08K3/18—Oxygen-containing compounds, e.g. metal carbonyls
    • C08K3/20—Oxides; Hydroxides
    • C08K3/22—Oxides; Hydroxides of metals
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00—Mixing; Kneading
    • B29B7/02—Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type
    • B29B7/06—Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices
    • B29B7/10—Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices rotary
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00—Mixing; Kneading
    • B29B7/80—Component parts, details or accessories; Auxiliary operations
    • B29B7/88—Adding charges, i.e. additives
    • B29B7/90—Fillers or reinforcements, e.g. fibres
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/022—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the choice of material
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/03—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
    • B29C48/09—Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels
    • B29C48/10—Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels flexible, e.g. blown foils
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25—Component parts, details or accessories; Auxiliary operations
    • B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/395—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders
    • B29C48/40—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders using two or more parallel screws or at least two parallel non-intermeshing screws, e.g. twin screw extruders
    • B29C48/402—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders using two or more parallel screws or at least two parallel non-intermeshing screws, e.g. twin screw extruders the screws having intermeshing parts
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25—Component parts, details or accessories; Auxiliary operations
    • B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/395—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders
    • B29C48/40—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders using two or more parallel screws or at least two parallel non-intermeshing screws, e.g. twin screw extruders
    • B29C48/405—Intermeshing co-rotating screws
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25—Component parts, details or accessories; Auxiliary operations
    • B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/395—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders
    • B29C48/40—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders using two or more parallel screws or at least two parallel non-intermeshing screws, e.g. twin screw extruders
    • B29C48/425—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders using two or more parallel screws or at least two parallel non-intermeshing screws, e.g. twin screw extruders using three or more screws
    • B29C48/43—Ring extruders
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25—Component parts, details or accessories; Auxiliary operations
    • B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/50—Details of extruders
    • B29C48/76—Venting, drying means; Degassing means
    • B29C48/765—Venting, drying means; Degassing means in the extruder apparatus
    • B29C48/766—Venting, drying means; Degassing means in the extruder apparatus in screw extruders
    • B29C48/767—Venting, drying means; Degassing means in the extruder apparatus in screw extruders through a degassing opening of a barrel
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25—Component parts, details or accessories; Auxiliary operations
    • B29C48/92—Measuring, controlling or regulating
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00—Use of inorganic substances as compounding ingredients
    • C08K3/34—Silicon-containing compounds
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2069/00—Use of PC, i.e. polycarbonates or derivatives thereof, as moulding material
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2509/00—Use of inorganic materials not provided for in groups B29K2503/00 - B29K2507/00, as filler
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2995/00—Properties of moulding materials, reinforcements, fillers, preformed parts or moulds
    • B29K2995/0018—Properties of moulding materials, reinforcements, fillers, preformed parts or moulds having particular optical properties, e.g. fluorescent or phosphorescent
    • B29K2995/003—Reflective
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00—Use of inorganic substances as compounding ingredients
    • C08K3/18—Oxygen-containing compounds, e.g. metal carbonyls
    • C08K3/20—Oxides; Hydroxides
    • C08K3/22—Oxides; Hydroxides of metals
    • C08K2003/2237—Oxides; Hydroxides of metals of titanium
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00—Use of inorganic substances as compounding ingredients
    • C08K3/18—Oxygen-containing compounds, e.g. metal carbonyls
    • C08K3/20—Oxides; Hydroxides
    • C08K3/22—Oxides; Hydroxides of metals
    • C08K2003/2237—Oxides; Hydroxides of metals of titanium
    • C08K2003/2241—Titanium dioxide
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00—Use of inorganic substances as compounding ingredients
    • C08K3/01—Use of inorganic substances as compounding ingredients characterized by their specific function
    • C08K3/013—Fillers, pigments or reinforcing additives
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L69/00—Compositions of polycarbonates; Compositions of derivatives of polycarbonates

Definitions

  • the present invention relates to a method for producing a molding composition with improved properties.
  • the present invention particularly relates to the production of a molding composition comprising a polycarbonate and a reinforcing filler.
  • this molding composition is obtainable by compounding a polycarbonate and the reinforcing filler with screw shafts arranged in a ring with one another by means of a multi-shaft extruder.
  • the reinforcing filler is preferably selected from one or more members of the group comprising the members titanium dioxide (TiO 2 ), talc (Mg 3 Si 4 O 10 (OH) 2 ), dolomite (CaMg [CO 3 ] 2 ), kaolinite (Al 4 [(OH) 8
  • the content of reinforcing filler is 3 to 50% by weight, based in each case on the total mass of the molding composition.
  • the content of reinforcing filler is preferably 10 to 35% by weight, particularly preferably 12 to 32% by weight, very particularly preferably 15 to 30% by weight, in each case based on the total mass of the molding composition.
  • these values apply to titanium dioxide (TiO 2 ) as a reinforcing filler, but also to other reinforcing fillers such as talc (Mg 3 Si 4 O 10 (OH) 2 ), dolomite CaMg [CO 3 ] 2 , kaolinite Al 4 [(OH) 8
  • the content of reinforcing filler is 15 to 45% by weight, particularly preferably 25 to 40% by weight, very particularly preferably 30 to 35% by weight, in each case based on the total mass of the molding composition.
  • these values apply to talc (Mg 3 Si 4 O 10 (OH) 2 ) as a reinforcing filler, but also to other reinforcing fillers such as titanium dioxide (TiO 2 ), dolomite (CaMg [CO 3 ] 2 ), kaolinite (Al 4 [(OH ) 8
  • polycarbonate, reinforcing filler and, if appropriate, other constituents can be introduced simultaneously or successively into the multi-screw extruder with screw shafts arranged in a ring with one another.
  • the reinforcing filler can be added either before the polycarbonate has melted or after the polycarbonate has melted.
  • the content of polycarbonate in the molding composition according to the invention is 97 to 55% by weight, in each case based on the total mass of the molding composition.
  • the polycarbonate content in the molding composition according to the invention is preferably 90 to 65% by weight, particularly preferably 88 to 68% by weight, very particularly preferably 85 to 70% by weight, in each case based on the total mass of the molding composition.
  • the content of reinforcing filler is 15 to 45% by weight, particularly preferably 25 to 40% by weight, very particularly preferably 30 to 35% by weight
  • the content of polycarbonate in the molding composition according to the invention is 85 to 55% by weight, particularly preferably 75 to 60% by weight, very particularly preferably 70 to 65% by weight, in each case based on the total mass of the molding composition.
  • the molding composition may also contain other ingredients.
  • the content of the other ingredients in the molding composition containing a polycarbonate and a reinforcing filler is from 0 to 37% by weight, preferably from 0 to 20% by weight, particularly preferably 0 to 10% by weight, in each case based on the total mass of Molding compound.
  • the sum of all components of the molding composition is 100% by weight.
  • a molding composition containing a polycarbonate is also called a polycarbonate molding composition below.
  • Improved dispersion of fillers in a polymer molding composition also has the effect, inter alia, that the molding composition has improved properties, in particular improved surface properties and improved mechanical properties such as e.g. has a higher toughness, a higher force absorption and greater elongation during the puncture test.
  • the object of the present invention is therefore to provide a method for producing an improved polycarbonate molding composition containing a reinforcing filler.
  • a process for producing a molding composition comprising a polycarbonate and a reinforcing filler, preferably selected from one or more members of the group comprising the members titanium dioxide (TiO 2 ) talc (Mg 3 Si 4 O 10 (OH ) 2 ), dolomite CaMg [CO 3 ] 2 , kaolinite Al 4 [(OH) 8
  • the content of reinforcing filler is 3 to 45% by weight, based in each case on the total mass of the polycarbonate molding composition.
  • the content of reinforcing filler is preferably 10 to 35% by weight, particularly preferably 12 to 32% by weight, very particularly preferably 15 to 30% by weight, in each case based on the total mass of the molding composition.
  • these values apply to titanium dioxide (TiO 2 ) as a reinforcing filler, but also to other reinforcing fillers such as talc (Mg 3 Si 4 O 10 (OH) 2 ), dolomite (CaMg [CO 3 ] 2 ), kaolinite (Al 4 [(OH ) 8
  • the content of reinforcing filler is 15 to 45% by weight, particularly preferably 25 to 40% by weight, very particularly preferably 30 to 35% by weight, in each case based on the total mass of the molding composition.
  • these values apply to talc (Mg 3 Si 4 O 10 (OH) 2 ) as a reinforcing filler, but also to other reinforcing fillers such as titanium dioxide (TiO 2 ), dolomite (CaMg [CO 3 ] 2 ), kaolinite (Al 4 [(OH ) 8
  • a reinforcing filler is understood to be a mineral filler which is suitable for increasing the rigidity of the polycarbonate molding composition produced in accordance with the invention.
  • Such a polycarbonate molding composition produced in accordance with the invention has better, i.e. improved, properties than polycarbonate molding compositions which have been produced using processes according to the prior art, the polycarbonate molding compositions which have been produced according to the prior art having the same constituents in the same proportions as the polycarbonate molding composition produced according to the invention.
  • molded body is understood to mean an object which is the result of further processing of the molding composition.
  • both an object obtainable from the molding compound by injection molding and a film or plate obtainable by extrusion of the molding compound are to be regarded as molded articles.
  • the modification rutile with a grain size d 50 of 0.1 ⁇ m to 5 ⁇ m, preferably 0.3 to 3 ⁇ m, is preferably used as titanium dioxide (TiO 2 ).
  • titanium dioxide which can be used according to the invention are selected from the products titanium dioxide Kronos which can be purchased 2230 and Kronos 2233 titanium dioxide; Kronos Titan GmbH Leverkusen is the manufacturer of both products.
  • Talc (Mg 3 Si 4 O 10 (OH) 2 ) is preferably used with a grain size d 50 of 0.1 ⁇ m to 10 ⁇ m, preferably 0.3 to 3 ⁇ m.
  • d 50 0.1 ⁇ m to 10 ⁇ m, preferably 0.3 to 3 ⁇ m.
  • Jetfine 3CA from Imerys Talc (Luzenac Europe SAS)
  • Talc HTP Ultra 5C from IMI Fabi SpA
  • the grain size dso is mass-related and was determined in accordance with ISO 1333 17-3 with a Sedigraph 5100 from Micrometrics, Germany.
  • Mixtures of titanium dioxide and talc can be used in any mixing ratio.
  • the mixing ratio of titanium dioxide to talc is preferably 1:60 to 1: 1, preferably 1:30 to 1: 5, in each case based on the mass.
  • the particles of the respective mineral that make up the reinforcing filler preferably have an aspect ratio of 1: 1 to 1: 7.
  • polycarbonate means both homopolycarbonates and copolycarbonates.
  • the polycarbonates can be linear or branched in a known manner. Mixtures of polycarbonates can also be used according to the invention.
  • Some, up to 80 mol%, preferably from 20 mol% to 50 mol%, of the carbonate groups in the polycarbonates used according to the invention can be replaced by preferably aromatic dicarboxylic acid ester groups.
  • Such polycarbonates which contain both acid residues of carbonic acid and acid residues of, preferably aromatic, dicarboxylic acids incorporated into the molecular chain, are referred to as aromatic polyester carbonates.
  • the carbonate groups are replaced by the aromatic dicarboxylic acid ester groups essentially stoichiometrically and also quantitatively, so that the molar ratio of the reactants is also found in the finished polyester carbonate.
  • the aromatic dicarboxylic acid ester groups can be incorporated either statistically or in blocks.
  • thermoplastic polycarbonates including the thermoplastic polyester carbonates, have average molecular weights Mw determined by GPC (gel permeation chromatography in methylene chloride with polycarbonate as standard) from 15 kg / mol to 50 kg / mol, preferably from 20 kg / mol to 35 kg / mol, particularly preferably from 23 kg / mol to 33 kg / mol.
  • GPC gel permeation chromatography in methylene chloride with polycarbonate as standard
  • the preferred aromatic polycarbonates and aromatic polyester carbonates are prepared in a known manner from diphenols, carbonic acid or carbonic acid derivatives and, in the case the polyester carbonates, preferably aromatic dicarboxylic acids or dicarboxylic acid derivatives, optionally chain terminators and branching agents.
  • aromatic polycarbonates and polyester carbonates takes place e.g. by reacting diphenols with carbonic acid halides, preferably phosgene, and / or with aromatic dicarboxylic acid dihalides, preferably benzenedicarboxylic acid dihalides, according to the phase interface method, optionally using chain terminators and optionally using trifunctional or more than trifunctional branching agents, part of the carbonic acid derivatives being used to prepare the polyester carbonates is replaced by aromatic dicarboxylic acids or derivatives of dicarboxylic acids, depending on the requirement of the carbonate structural units to be replaced in the aromatic polycarbonates, by aromatic dicarboxylic acid ester structural units. It is also possible to use a melt polymerization process by reacting diphenols with, for example, diphenyl carbonate.
  • Dihydroxyaryl compounds suitable for the preparation of polycarbonates are those of the formula (1) HO-Z-OH (1), in which Z is an aromatic radical having 6 to 30 carbon atoms, which may contain one or more aromatic nuclei, may be substituted and may contain aliphatic or cycloaliphatic radicals or alkylaryls or heteroatoms as bridge members.
  • X is preferably a single bond, C1- to C5-alkylene, C2- to C5-alkylidene, C5- to C6-cycloalkylidene, -O-, -SO-, -CO-, -S-, -SO2- or for a radical of the formula (2a)
  • Diphenols suitable for the preparation of the polycarbonates are, for example, hydroquinone, resorcinol, dihydroxydiphenyls, bis (hydroxyphenyl) alkanes, bis (hydroxyphenyl) cycloalkanes, bis (hydroxyphenyl) sulfides, bis (hydroxyphenyl) ethers, bis ( hydroxyphenyl) ketones, bis (hydroxyphenyl) sulfones, bis (hydroxyphenyl) sulfoxides, ⁇ - ⁇ '-bis (hydroxyphenyl) diisopropylbenzenes, phthalimidines derived from isatin or phenolphthalein derivatives and their nuclear alkylated, nuclear arylated and nuclear halogenated compounds.
  • Preferred diphenols are 4,4'-dihydroxydiphenyl, 2,2-bis (4-hydroxyphenyl) propane (bisphenol A), 2,4-bis (4-hydroxyphenyl) -2-methylbutane, 1,1-bis- (4-hydroxyphenyl) -p-diisopropylbenzene, 2,2-bis (3-methyl-4-hydroxyphenyl) propane, dimethyl bisphenol A, bis (3,5-dimethyl-4-hydroxyphenyl) methane, 2 , 2-bis (3,5-dimethyl-4-hydroxyphenyl) propane, bis (3,5-dimethyl-4-hydroxyphenyl) sulfone, 2,4-bis (3,5-dimethyl-4- hydroxyphenyl) -2-methylbutane, 1,1-bis (3,5-dimethyl-4-hydroxyphenyl) -p-diisopropylbenzene and 1,1-bis (4-hydroxyphenyl) -3,3,5-trimethylcyclohexane.
  • diphenols are 2,2-bis (4-hydroxyphenyl) propane (bisphenol A), 2,2-bis (3,5-dimethyl-4-hydroxyphenyl) propane, 1,1-bis (4 -hydroxyphenyl) -cyclohexane, 1,1-bis- (4-hydroxyphenyl) -3,3,5-trimethylcyclohexane and dimethyl-bisphenol A.
  • diphenols are, for example, in US-A 3,028,635 , US-A 2 999 825 , US-A 3 148 172 , US-A 2 991 273 , US-A 3,271,367 , US-A 4,982,014 and US-A 2 999 846 , in DE-A 1 570 703 , DE-A 2063 050 , DE-A 2 036 052 , DE-A 2 211 956 and DE-A 3 832 396 , in FR-A 1 561 518 , in the monograph " H. Schnell, Chemistry and Physics of Polycarbonates, Interscience Publishers, New York 1964 " as in JP-A 62039/1986 , JP-A 62040/1986 and JP A 105550/1986 described.
  • Suitable carbonic acid derivatives are, for example, phosgene or diphenyl carbonate.
  • Suitable chain terminators that can be used in the production of the polycarbonates are monophenols.
  • Suitable monophenols are, for example, phenol itself, alkylphenols such as cresols, p-tert-butylphenol, cumylphenol and mixtures thereof.
  • Preferred chain terminators are the phenols which are mono- or polysubstituted by C1 to C30 alkyl, linear or branched, preferably unsubstituted, or substituted by tert-butyl. Particularly preferred chain terminators are phenol, cumylphenol and / or p-tert-butylphenol.
  • the amount of chain terminator to be used is preferably 0.1 to 5 mol%, based on moles of diphenols used in each case.
  • the chain terminators can be added before, during or after the reaction with a carbonic acid derivative.
  • Suitable branching agents are the tri- or more than trifunctional compounds known in polycarbonate chemistry, in particular those with three or more than three phenolic OH groups.
  • Suitable branching agents are, for example, 1,3,5-tri- (4-hydroxyphenyl) benzene, 1,1,1-tri- (4-hydroxyphenyl) ethane, tri- (4-hydroxyphenyl) phenylmethane, 2,4- Bis (4-hydroxyphenylisopropyl) phenol, 2,6-bis (2-hydroxy-5'-methylbenzyl) -4-methylphenol, 2- (4-hydroxyphenyl) -2- (2,4-dihydroxyphenyl) propane, tetra (4-hydroxyphenyl) methane, tetra (4- (4-hydroxyphenylisopropyl) phenoxy) methane and 1,4-bis ((4 ', 4 "-dihydroxytriphenyl) methyl) benzene and 3,3-bis (3-methyl-4-hydroxyphenyl) -2-oxo-2,3-dihydroindole.
  • the amount of branching agents which may be used is preferably 0.05 mol% to 2.00 mol%, based on moles of diphenols used in each case.
  • the branching agents can either be introduced with the diphenols and the chain terminators in the aqueous alkaline phase or added in solution in an organic solvent before the phosgenation. In the case of the transesterification process, the branching agents are used together with the diphenols.
  • Particularly preferred polycarbonates are the homopolycarbonate based on bisphenol A, the homopolycarbonate based on 1,3-bis (4-hydroxyphenyl) -3,3,5-trimethylcyclohexane and the copolycarbonates based on the two monomers bisphenol A and 1.1 -Bis (4-hydroxyphenyl) -3,3,5-trimethylcyclohexane.
  • Preferred methods of production of the polycarbonates to be used according to the invention, including the polyester carbonates, are the known interfacial process and the known melt transesterification process (cf. e.g. WO 2004/063249 A1 , WO 2001/05866 A1 , WO 2000/105867 , US 5,340,905 A , US 5,097,002 A , US-A 5,717,057 A. ).
  • polycarbonate is aromatic polycarbonate based on bisphenol A.
  • titanium dioxide TiO 2
  • talc Mg 3 Si 4 O 10 (OH) 2
  • dolomite CaMg [CO 3 ] 2
  • kaolinite Al 4 [(OH) 8
  • wollastonite Ca 3 [Si 3 O 9 ]
  • the content of the other ingredients in the polycarbonate molding composition produced according to the invention is from 0 to 37% by weight, preferably from 0 to 20% by weight, particularly preferably 0 to 10% by weight.
  • ingredients that are neither polycarbonate nor reinforcing filler are ingredients that are neither polycarbonate nor reinforcing filler.
  • these other ingredients are, in particular, ingredients that are neither polycarbonate nor titanium dioxide (TiO 2 ), talc (Mg 3 Si 4 O 10 (OH) 2 ), dolomite (CaMg [CO 3 ] 2 ), kaolinite (Al 4 [(OH) 8
  • thermoplastics for example acrylonitrile-butadiene-styrene copolymers, or other additives such as UV stabilizers, IR stabilizers, thermal stabilizers, antistatic agents, dyes and pigments are added in the customary amounts; if necessary, the demolding behavior, the flow behavior and / or the flame resistance can be improved by adding external mold release agents, flow agents, and / or flame retardants (e.g. alkyl and aryl phosphites, phosphates, phosphines, low molecular weight carboxylic acid esters, halogen compounds, salts) Chalk Quartz flour, glass and carbon fibers, pigments and their combination.
  • flame retardants e.g. alkyl and aryl phosphites, phosphates, phosphines, low molecular weight carboxylic acid esters, halogen compounds, salts
  • Chalk Quartz flour glass and carbon fibers, pigments and their combination.
  • Such connections are e.g.
  • Suitable additives are described, for example, in “ Additives for Plastics Handbook, John Murphy, Elsevier, Oxford 1999”, in the “ Plastics Additives Handbook, Hans Doubt, Hanser, Kunststoff 2001 ".
  • Suitable antioxidants or thermal stabilizers are, for example: Alkylated monophenols, alkylthiomethylphenols, hydroquinones and alkylated hydroquinones, tocopherols, hydroxylated thiodiphenyl ethers, alkylidene bisphenols, O-, N- and S-benzyl compounds, hydroxybenzylated malonates, aromatic hydroxybenzyl compounds, triazine compounds, acylaminophenols, esters of ⁇ - (3,5- butyl-4-hydroxyphenyl) propionic acid, esters of ⁇ - (5-tert-butyl-4-hydroxy-3-methylphenyl) propionic acid, esters of ⁇ - (3,5-dicyclohexyl-4-hydroxyphenyl) propionic acid, esters of 3, 5-di-tert-butyl-4-hydroxyphenylacetic acid, amides of ⁇ - (3,5-di-tert-butyl-4-hydroxyphenyl) propionic
  • Organic phosphites, phosphonates and phosphanes are preferred, mostly those in which the organic radicals consist wholly or partly of optionally substituted aromatic radicals.
  • Suitable complexing agents for heavy metals and for neutralizing traces of alkali are o / m phosphoric acids, fully or partially esterified phosphates or phosphites.
  • Suitable light stabilizers are 2- (2'-hydroxyphenyl) benzotriazoles, 2-hydroxybenzophenones, esters of substituted and unsubstituted benzoic acids, acrylates, sterically hindered amines, oxamides and 2- (hydroxyphenyl) -1,3,5- triazines or substituted hydroxyalkoxyphenyl, 1,3,5-triazoles, substituted benzotriazoles such as, for. B.
  • Polypropylene glycols alone or in combination with e.g. B. sulfones or sulfonamides as stabilizers can be used against damage by gamma rays.
  • Processing aids such as mold release agents, usually derivatives of long-chain fatty acids, can also be added.
  • Z are preferred.
  • Suitable flame retardant additives are phosphate esters, i.e. H. Triphenyl phosphate, resorcinol diphosphate, bromine-containing compounds such as brominated phosphoric esters, brominated oligocarbonates and polycarbonates, and preferably salts of fluorinated organic sulfonic acids.
  • Suitable impact modifiers are butadiene rubber with grafted-on styrene-acrylonitrile or methyl methacrylate, ethylene-propylene rubbers with grafted-on maleic anhydride, ethyl- and butyl-acrylate rubbers with grafted-on methyl methacrylate or styrene-acrylonitrile, interpenetrating siloxane-acrylate-acrylate or acrylate-nitrate-networks or acrylate-acrylate-acrylate-acrylate-or acrylate-nitrate networks with acrylate or acrylate-acrylate.
  • colorants such as organic dyes or pigments or inorganic pigments, IR absorbers, individually, in a mixture or in combination with stabilizers, glass fibers, glass (hollow) spheres, inorganic, in particular mineral, fillers can be added.
  • polycarbonate molding composition according to the invention optionally in a mixture with other thermoplastics and / or customary additives, can be used wherever known polycarbonate molding compositions are used.
  • a multi-screw extruder with screw shafts arranged in a ring shape has 8 to 16, usually 10 or 12 screw shafts rotating in the same direction.
  • the worm shafts are equipped with worm elements, which are preferably closely intermeshing with respect to the respectively directly adjacent worm elements of the respectively directly adjacent worm shafts.
  • the worm shafts are arranged in a ring around an inner core with a contour adapted to the worm shafts occupied by the worm elements.
  • Each worm shaft is immediately adjacent to two other worm shafts. On the outside, these worm shafts are surrounded by an outer housing, the inner contour of which is also adapted to the worm shafts.
  • the housing and / or the core of the multi-shaft extruder with screw shafts arranged in a ring with respect to one another can be designed to be both heatable and coolable.
  • such a multi-shaft extruder with screw shafts arranged in a ring shape with respect to one another is also referred to below as ring extruder.
  • the screw elements of a ring extruder do not differ from those of a twin screw extruder, which is faced with the same process engineering task.
  • the process zones of a ring extruder do not differ from those of a twin-screw extruder, which is faced with the same process engineering task.
  • the outside diameter of a tightly intermeshing screw element is also referred to as a DA.
  • the core radius of such a screw element is referred to as DI.
  • the L / D ratio is the quotient of the length of the section of the screw shaft which is occupied by screw elements and the outer diameter of a tightly intermeshing screw element which cleans the inner wall of the extruder.
  • Ring extruders in and of themselves are known for example from: DE4412725A1 , DE4412741A1 , DE19622582A1 , DE202007004997U1 , DE202007005010U1 , WO03020493A1 and WO2006045412A2 as well as from the publication " Compounding with twelve waves “Carl Hanser Verlag, Kunststoff, KU Kunststoffe, year 90 (2000) 8, pages 60 to 62 .
  • a method for producing a polycarbonate molding composition containing a reinforcing filler preferably selected from one or more members of the group comprising the members titanium dioxide (TiO 2 ), talc (Mg 3 Si 4 O 10 (OH) 2 ), Dolomite (CaMg [CO 3 ] 2 ), kaolinite (Al 4 [(OH) 8
  • the content of reinforcing filler is preferably 10 to 35% by weight, particularly preferably 12 to 32% by weight, very particularly preferably 15 to 30% by weight, in each case based on the total mass of the molding composition.
  • these values apply to titanium dioxide (TiO 2 ) as a reinforcing filler, but also for other reinforcing fillers such as talc (Mg 3 Si 4 O 10 (OH) 2 ), dolomite (CaMg [CO 3 ] 2 ), kaolinite (Al 4 [(OH) 8
  • the content of reinforcing filler is 15 to 45% by weight, particularly preferably 25 to 40% by weight, very particularly preferably 30 to 35% by weight, in each case based on the total mass of the molding composition.
  • these values apply to talc (Mg 3 Si 4 O 10 (OH) 2 ) as a reinforcing filler, but also to other reinforcing fillers such as titanium dioxide (TiO 2 ), dolomite (CaMg [CO 3 ] 2 ), kaolinite (Al 4 [(OH ) 8
  • Such a polycarbonate molding composition produced in accordance with the invention has better properties than polycarbonate molding compositions which are compared to polycarbonate molding compositions which have been produced by processes according to the prior art, the polycarbonate molding compositions which have been produced according to the prior art having the same constituents in the same proportions as that Polycarbonate molding composition produced according to the invention.
  • a ring extruder with 10 or 12 screw shafts is preferably used, and a ring extruder with 12 screw shafts is particularly preferably used.
  • the ring extruder has an L / D ratio of 28 to 45, particularly preferably 33 to 42.
  • the ring extruder has a DA / DI ratio of 1.5 to 1.8, particularly preferably of 1.55 to 1.74.
  • the ring extruder has a torque density of 2 to 10 Nm / cm 3 , preferably 4 to 8 Nm / cm 3 , particularly preferably 5.5 to 6.5 Nm / cm 3 , the torque density being defined as Quotient of the maximum torque of a worm shaft divided by the third power of the center distance of two neighboring worm shafts.
  • the screw elements of the ring extruder have an outside diameter DA of 10 to 100 mm.
  • the ring extruder has a passage depth, defined as (DA - DI) / 2, of 2 to 40 mm.
  • the ring extruder has a free cross-sectional area of 5 to 1000 cm 2 .
  • the free cross-sectional area is the area of the extruder bore that is not filled by screw elements or extruder shaft, that is to say is available for conveying the polycarbonate molding compound.
  • the ring extruder used according to the invention can be, for example, one of the ring extruders with the names RingExtruder RE® 3 XP, RingExtruder RE® 1 XPV or RingExtruder RE® 3 XPV from Extricom Extrusion GmbH.
  • the present invention also relates to a molding composition which is produced by the process according to the invention.
  • Another object of the invention is the use of the molding composition according to the invention for the production of reflectors in lights or structural components, for example for automobile construction.
  • the experiments described in Examples 1-3 were carried out using a ZE60A UTXi twin-screw extruder from KraussMaffei Berstorff GmbH.
  • the twin-screw extruder used has an inside diameter of 65 mm and an L / D ratio of 43.
  • the basic structure of the extruder used shows Figure 1 .
  • the twin-screw extruder has a housing consisting of 11 parts, in which two co-rotating shafts (not shown) are arranged which rotate in the same direction.
  • Example 1 all the components of the polycarbonate molding composition were metered in via the main intake in housing 2 via the intake funnel 1 shown.
  • the housing part 11 there is the degassing opening 13 which is connected to a suction device (not shown).
  • plasticizing zone which consists of different two- and three-course kneading blocks of different widths and tooth blocks.
  • a mixing zone which consists of kneading elements, tooth blocks and conveying elements.
  • the pressure build-up zone is located in housing 12, followed by melt filtration (position A1 in Figure 1 ) (Type: DSC 176 from Maag) and then a nozzle plate with 29 holes.
  • the polycarbonate granules were metered in via the main feed in housing 2 via the feed funnel 1 shown.
  • the titanium dioxide powder was metered into housing 8 via a side feed device.
  • the degassing opening 13 In the housing part 11 there is the degassing opening 13, which is connected to a suction device (not shown).
  • Conveying zones for the polycarbonate granulate are located in the area of the housings 2 to 5.
  • plasticizing zone which consists of different two- and three-course kneading blocks of different widths and tooth blocks.
  • a mixing zone which consists of kneading elements, tooth blocks and conveying elements.
  • the pressure build-up zone is located in housing 12, followed by melt filtration (position A1 in Figure 1 ) (Type: DSC 176 from Maag) and then a nozzle plate with 29 holes.
  • Example 3 all the components of the polycarbonate molding composition were metered in via the main intake in housing 2 via the intake funnel 1 shown.
  • the housing part 11 there is the degassing opening 13 which is connected to a suction device (not shown).
  • Conveying zones for the polycarbonate granules and the titanium dioxide powder are located in the area of the housings 2 to 7.
  • plasticizing zone which consists of different two- and three-course kneading blocks of different widths and tooth blocks.
  • the pressure build-up zone is located in housing 12, followed by melt filtration (position A1 in Figure 1 ) (Type: DSC 176 from Maag) and then a nozzle plate with 29 holes.
  • Example 2 the polycarbonate granules were metered into the feed hopper 1 using a commercially available gravimetric differential metering scale.
  • the titanium dioxide powder was metered into a housing 8 by means of a commercially available gravimetric differential metering scale via a side feeding device.
  • Example 1 the granulation was carried out as strand granulation after water bath cooling.
  • melt temperature was measured by inserting a thermocouple into the emerging melt of the middle melt strand directly in front of the nozzle.
  • Example 4 The test described in Example 4 (according to the invention) was carried out using a multi-screw extruder of the ring extruder type RE 3XP from Extricom GmbH.
  • the multi-shaft extruder used has 12 shafts, each with an outer screw diameter of 30 mm, a DA / DI ratio of 1.55 and an L / D ratio of 39.
  • the basic structure of the extruder used shows Figure 2 .
  • the multi-shaft extruder has a housing consisting of 12 parts, in which 12 co-rotating shafts (not shown) are arranged which rotate in the same direction.
  • Conveying zones for the polycarbonate granules and the titanium dioxide powder are located in the area of the housings 15 to 19.
  • plasticizing zone which consists of various two-course kneading blocks of different widths and tooth mixing elements.
  • a mixing zone which consists of various conveying and mixing elements.
  • the pressure build-up zone is located in housing 26, followed by melt filtration (position A2 in Figure 2 ) (Type K-SWE-121 from Kreyenborg) and then a nozzle plate with 24 holes.
  • Example 4 polycarbonate granules and titanium dioxide powder were metered into the feed hopper 14 using commercially available gravimetric differential metering scales.
  • the granulation was carried out as strand granulation after water bath cooling.
  • the melt temperature was measured by inserting a thermocouple into the emerging melt in one of the two middle melt strands directly in front of the nozzle.
  • Example 5 The test described in Example 5 was carried out using a ZE60A UTXi twin-screw extruder from KraussMaffei Berstorff GmbH.
  • the twin-screw extruder used has an inside diameter of 65 mm and an L / D ratio of 43.
  • the basic structure of the extruder used shows Figure 3 .
  • the twin-screw extruder has a housing consisting of 11 parts, in which two co-rotating shafts (not shown) are arranged which rotate in the same direction.
  • Example 5 all the components of the polycarbonate molding composition were metered via the main intake in housing 29 via the intake funnel 28 shown.
  • housing part 38 there is the degassing opening 40, which is connected to a suction device (not shown).
  • Conveying zones for the polycarbonate granules and the titanium dioxide powder are located in the area of the housings 30 to 32.
  • plasticizing zone which consists of different two- and three-course kneading blocks of different widths and tooth blocks.
  • a mixing zone which consists of kneading elements, tooth blocks and conveying elements.
  • the pressure build-up zone is located in housing 39 and is followed by a nozzle plate with 29 holes.
  • polycarbonate granules and titanium dioxide powder were metered into the feed hopper 28 by means of commercially available gravimetric differential metering scales.
  • the granulation was carried out as strand granulation after water bath cooling.
  • the melt temperature was measured by inserting a thermocouple into the emerging melt of the middle melt strand directly in front of the nozzle.
  • the experiments described in Examples 6 to 8 were carried out with a multi-screw extruder of the ring extruder type RE 1XPV from Extricom GmbH.
  • the multi-shaft extruder used has 12 shafts, each with an outer screw diameter of 18.7 mm, a DA / DI ratio of 1.74 and an L / D ratio of 35.
  • the basic structure of the extruder used shows Figure 4 .
  • the multi-shaft extruder has a housing consisting of 7 parts, in which 12 co-rotating shafts (not shown) meshing with one another are arranged.
  • the polycarbonate granules were metered in via the main feed in housing 42 via the feed funnel 41 shown.
  • the titanium dioxide powder was metered into housing 45 via a side feed device.
  • the degassing opening 49 is located in the housing part 47 and is connected to a suction device (not shown).
  • plasticizing zone which consists of different two-course kneading blocks of different widths.
  • mixing zones which consist of kneading elements, tooth blocks and conveying elements.
  • the pressure build-up zone is located in housing 48 and is followed by a nozzle plate with 7 holes.
  • the polycarbonate granules were metered into the feed hopper 41 using a commercially available gravimetric differential metering scale.
  • the titanium dioxide powder was metered into a housing 45 by means of a commercially available gravimetric differential metering scale via a side feeding device.
  • the granulation was carried out as strand granulation after water bath cooling.
  • the melt temperature was measured by inserting a thermocouple into the emerging melt in the middle melt strand directly in front of the nozzle.
  • the polycarbonate composition produced in Examples 5 to 8 was subsequently processed into test specimens with a length and width of 60 mm and a thickness of 2 mm using an injection molding process.
  • Injection molding was carried out under the following process conditions characteristic of polycarbonates: melt temperature: 310 ° C, mold temperature: 90 ° C. Before the injection molding processing, the granules of the polycarbonate molding composition were predried at 110 ° C. within 4 hours.
  • the dispersion quality of the titanium dioxide powder was determined by means of visual evaluation of extruded foils.
  • 150 ⁇ m thick films were produced from the granules of the polycarbonate molding composition using a film extrusion system, consisting essentially of a single-screw extruder followed by a rolling mill. These foils were then photographed on a commercially available light table in transmitted light with a scale applied using a camera. The photos (see Figures 5 to 12 ) were then assessed visually and divided into grades 1 (excellent) to 6 (poor) (see Table 2). For all Figures 5 to 12 applies: scale: 1 graduation corresponds to 1 mm; incompletely dispersed titanium dioxide particles can be seen as dark spots in the image.
  • Comparative examples 1 and 3 differ in the speed of the extruder. While in example 1 the extruder speed is 300 1 / min, in example 3 it is twice as high with the same throughput of 580 kg / h.
  • the increase in speed leads to a significantly better dispersion, as can be seen from the significantly lower pressure increase upstream of the melt sieve (see Table 1) and the lower number of undispersed titanium dioxide particles (see Figure 5 (Example 1) compared to Figure 6 (Example 2)) can recognize.
  • the melt temperature at the higher speed in Example 3 simultaneously increases by 34 ° C., which promotes polymer degradation in a manner known to the person skilled in the art.
  • Comparative examples 1 and 2 differ only in the metering point of the titanium dioxide powder. While in example 1 the titanium dioxide powder was added to the feed hopper 1, the addition in example 2 was carried out after melting in a side feed device in housing 8 into the polycarbonate melt. As can be seen in Table 1, the addition of the titanium dioxide powder after melting in Example 2 leads to a significantly higher pressure increase before the melt sieve, which is a sign of poorer dispersion, as well Figure 7 confirmed which shows a large number of very poorly dispersed titanium dioxide particles. In comparison, in Figure 5 (Example 1) the number of large titanium dioxide particles significantly lower.
  • Example 4 was to achieve an at least comparable titanium dioxide dispersion as in Comparative Example 3, but with a significantly lower melt temperature.
  • a structure as well as a throughput and a speed of the method according to the invention were selected, which led to a comparable pressure increase upstream of the melt sieve as in comparative example 3.
  • the titanium dioxide was in each case via the feed hopper 1 and 14 added to the extruder.
  • example 4 according to the invention shows that the method according to the invention made it possible to achieve a significantly better dispersion of the titanium dioxide particles with a simultaneously low melt temperature.
  • This can be recognized on the one hand by the fact that the pressure increase in example 4 is as high as in example 3, but the melt temperature is 35 ° C. lower (see table 1).
  • Figure 8 to recognize that the number of poorly dispersed titanium dioxide particles comparable to Example 3 ( Figure 6 ), but less than in Example 1 ( Figure 5 ).
  • the titanium dioxide powder was added via the feed hopper 28 into a co-rotating twin-screw extruder.
  • the dispersion quality of the titanium dioxide was determined by visual determination of the size and number of the incompletely dispersed titanium dioxide particles in a film produced as described above (see Figure 9 ).
  • the multiaxial mechanical properties were determined using a puncture test as described above in accordance with DIN EN ISO 6603-2: 2000 at 23 ° C.
  • the titanium dioxide powder was added in housing 45 after the polycarbonate had melted.
  • this procedure had the effect that the dispersion of the titanium dioxide particles was significantly worse than when added to the first extruder housing (see pressure increase in Table 1 and resulting particle sizes in Figure 7 ).
  • the puncture test on samples from example 6 according to the invention shows a significantly higher mathematical product of maximum deformation and maximum force than in comparative example 5 (see table 1).
  • the visual evaluation of the film also results in better dispersion of the titanium dioxide particles in Example 6 according to the invention compared to Example 5. This illustrates that the method according to the invention improves the dispersion of the titanium dioxide particles even when the titanium dioxide powder is not optimally added, that is to say after the polycarbonate has melted leads to better mechanical properties.
  • Example 6 a melt temperature which was 44 ° C. lower was achieved in Example 6 according to the invention than in Comparative Example 5 (see Table 1).
  • Example 7 20% by weight of titanium dioxide powder was added in housing 45 after the polycarbonate had melted. Despite the fact that the addition point of the titanium dioxide is not optimal in comparison to the comparative example 5 and the simultaneously higher amount of titanium dioxide, which is known to lead to embrittlement of the polycarbonate molding compound, only a slightly lower mathematical product of maximum deformation and maximum force was measured than in the comparative example (see table 1 ).
  • the visual assessment of the titanium dioxide particle dispersion using the films shows that the films made from the polycarbonate molding composition according to the invention from Example 7 (see Figure 11 ) have better titanium dioxide dispersion than the films made from the polycarbonate molding composition of Comparative Example 5 (see Figure 9 ). Even with the higher titanium dioxide content, the melt temperature is 42 ° C lower than in Comparative Example 5 (see Table 1).
  • Example 8 30% by weight of titanium dioxide powder was added in housing 45 after the polycarbonate had melted.
  • the addition point of the titanium dioxide which is not optimal in comparison to comparative example 5, and the simultaneously higher amount of titanium dioxide, which is known to lead to embrittlement of the polycarbonate molding composition, only a smaller decrease in the mathematical product from maximum deformation and maximum force was found than is known from comparable products is (see Table 1).
  • the visual assessment of the titanium dioxide particle dispersion using the films shows that the films made from the polycarbonate molding composition according to the invention from Example 8 (see Figure 12 ) have approximately the same good titanium dioxide dispersion as the films made from the polycarbonate molding composition of Comparative Example 5 (see Figure 9 ).

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